CN1524806A - Treating method suitable for presumption of recycling pure water into circulating water system - Google Patents
Treating method suitable for presumption of recycling pure water into circulating water system Download PDFInfo
- Publication number
- CN1524806A CN1524806A CNA031053947A CN03105394A CN1524806A CN 1524806 A CN1524806 A CN 1524806A CN A031053947 A CNA031053947 A CN A031053947A CN 03105394 A CN03105394 A CN 03105394A CN 1524806 A CN1524806 A CN 1524806A
- Authority
- CN
- China
- Prior art keywords
- accordance
- water
- acid
- sterilant
- circulating water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
A method of handling reclaiming assumed pure water for circulating water system comprising the steps of, removing oil from the assumed pure water, depositing, introducing into the circulating water system, charging inorganic alkaline substance to make the pH of cycle water to be 7.0-11, charging germicidal agent and antisludging agent, wherein the alkaline substance is a mixture of two or more selected from NaOH, KOH, Na2Co3, K2Co3, NaiHCo3, and KHCO3, While the bactericidal agent is a mixture two or more selected from chlorine, sodium hypochlorite, potassium hypochlorite, calcium hypochlorite, dichloroisocyanuric acid, trichloroiminocyanuric acid, chlorine dioxide, bromine, sodium hypochlorite, potassium hypochlorite, calcium hypochlorite, and quaternary ammonium salt.
Description
Technical field
The present invention relates to the treatment process that a kind of suitable supposition water purification is back to circulating water system, exactly, is burn into fouling and the microbial reproduction method that is used to suppress to suppose after water purification is back to circulating water system.
Technical background
The said supposition water purification of the present invention is meant the high oil-containing muddy water between industrial sewage and fresh water that pump water coolant in the refining of petroleum enterprise, the flushing surface water, rainwater etc. form.The principal feature of water quality is: compare the oleaginousness height with fresh water, the suspension object height; Compare with industrial sewage, salts contg is low, and other organic content is few.Water quality generally can reach discharging standards after oil removal, sedimentation.If the sewage draining exit downstream does not have particular requirement to sewer, suppose that water purification generally directly effluxes after oil removal, sedimentation; If there is aquatic organism plant in the discharge outlet downstream, suppose that water purification generally advances waste disposal plant again and handles after oil removal, sedimentation.
Industrial enterprise faces water saving and reduces wastewater disposition, improves the problem of enterprise's overall economic efficiency simultaneously, therefore, is a kind of highly effective method with sewage recycling.Suppose that water purification generally accounts for 30% of refining of petroleum enterprise sewage total amount, to suppose that water purification does not advance waste disposal plant after the oil removal sedimentation, direct reuse is in circulating water system, can make the sewage load of waste disposal plant reduce 20～30% on the one hand, save the construction cost of sewage disposal expense and waste disposal plant; To save fresh water consumption about 30% for enterprise on the other hand, reduces wastewater disposition about 30% simultaneously.
The U.S. is realizing discharging urban sewage recycling 60 years 20th century in the power generation cycle water system, and the nineties has realized that the qualified discharge industrial sewage is back to the petrochemical equipment circulating water system.The method of taking is that sewage is carried out advanced treatment, reduces COD, suspended substance and microorganism concn in the qualified discharge industrial sewage, uses the corrosion and the fouling of water conditioner operating device again, adopts continuous chlorination or with the microorganism in the bromine oxygen Control Circulation water.The treatment effect of this treatment process is better, and erosion rate adheres to speed less than 15mg/cm less than 0.075mm/a
2.mon., the recirculated water microorganism can be controlled in 10
4Individual/as below the mL, can to realize on the one hand reusing sewage can satisfying industrial production to the circulating water treatment effect of requirement simultaneously in circulating water system.
CN1338433 has proposed a kind ofly to handle sewage direct reuse up to standard in recirculated water with chemical process, adopts to add sterilant and corrosion inhibiting and descaling agent continuously, and treatment effect can satisfy the requirement of production equipment, and has realized industrialization.
But up to the present, refining of petroleum enterprise enters waste disposal plant with the supposition water purification to handle or directly efflux after oil removal, sedimentation, will not suppose that as yet water purification is back to circulating water system.Major cause is to suppose water purification after the oil removal sedimentation, though oleaginousness and suspended substance can reach discharging standards in the ordinary course of things in the water, but still does not reach conventional water technology to requirements in water quality.Petroleum hydrocarbon in the water increases the control difficulty of microorganism, and suspended substance increases the corrodibility of water quality, adopts the treatment effect of conventional water technology can not satisfy the requirement of production equipment.
Summary of the invention
The object of the present invention is to provide a kind of simple, effective, economic supposition water purification to be back to the treatment process of circulating water system, solving the supposition water purification is back to after the circulating water system microbial reproduction and biological clay and grows and be difficult to control, problems such as interchanger corrosion and fouling aggravation.
Supposition water purification provided by the invention is back to the circulating water system treatment process and comprises: will suppose that water purification introduces circulating water system after oil removal, sedimentation, adding inorganic base substance makes recirculated water pH value reach 7.0～11, add sterilant and corrosion inhibiting and descaling agent, make its concentration in recirculated water be controlled at 1～100mg/L and 2.0～50mg/L respectively.
The said alkaline matter of the present invention can be selected from NaOH, KOH, Na
2CO
3, K
2CO
3, NaHCO
3, KHCO
3One of or two or more mixture wherein.Preferred NaHCO
3, adding concentration is 20～1000mg/L, preferred 50～500mg/L; Recirculated water pH value is controlled at 7.0～11, and preferred 7.5～10.0.
The said sterilant of the present invention can be selected from one of chlorine, clorox, potassium hypochlorite, Losantin, DICHLOROISOCYANURIC ACID, trichloroisocyanuric acid, dioxide peroxide, bromine, sodium hypobromite, potassium hypobromite, hypobromous acid calcium, quaternary ammonium salt and quaternary alkylphosphonium salt or two or more mixture wherein.Preferred clorox or DICHLOROISOCYANURIC ACID or trichloroisocyanuric acid, adding concentration is 1～100mg/L, preferred 2～50mg/L.
When being back to recirculated water with the inventive method processing supposition water purification, if add corrosion inhibiting and descaling agent continuously, corrosion of carbon steel speed can be controlled at below the 0.075mm/a, adheres to speed and can be controlled at 20mg/cm
2.mon. in.Said corrosion inhibiting and descaling agent can be a hydroxyl phosphino-acetate, 1-Hydroxy Ethylidene-1,1-Diphosphonic Acid, and Sodium hexametaphosphate 99, zinc salt, molybdate etc., preferred hydroxyl phosphino-acetate, adding concentration is 1～50mg/L, preferred 3～15mg/L.
When handling the supposition water purification and be back to recirculated water, need continuously or be interrupted adding sterilant with the inventive method, can Control Circulation water microorganism concentration 10
5Individual/below the mL.
Adopt the inventive method to handle the supposition water purification, can make the supposition water purification after oil removal, sedimentation be back to circulating water system.Not only save precious water resource, and can effectively suppress the burn into fouling and the microbial reproduction of circulating water system.This method is simple to operate, and processing costs is low, is convenient to industrial implementation.
Embodiment
Embodiment 1
Present embodiment is the rotary hanging plate corrosion test, carries out with reference to HG/T2159-91.
Test water quality: test water is the scene supposition water purification of certain refinery after oil removal, sedimentation, main water quality data such as table 1.
The main water quality of certain refinery supposition water purification of table 1
| Project | Unit | Data |
| PH turbidity suspension petroleum-type ammonia nitrogen COD sulfide volatile phenol total hardness total alkalinity is total molten solid | ? ????mg/L ????mg/L ????mg/L ????mg/L ????mg/L ????mg/L ????mg/L ????mg/L ????mg/L ????mg/L | ????6.0 ????10.4 ????22.7 ????14.5 ????0.4 ????37.0 ????0.07 ????0.01 ????156.5 ????94.7 ????218.7 |
The NaHCO that in test water, adds different concns
3The pH value is adjusted to 8.0, add copolymer, the 5mg/L zinc chloride of 5mg/L 1-Hydroxy Ethylidene-1,1-Diphosphonic Acid, 5mg/L hydroxyl phosphine carboxylic acid, 5mg/L vinylformic acid and AMPS again, the erosion rate of rotary hanging plate is 0.026mm/a, and the erosion rate that does not add the rotary hanging plate of above-mentioned medicament is 1.32mm/a.
Embodiment 2
Present embodiment is the rotary hanging plate corrosion test, carries out with reference to HG/T2159-91.
Test water quality is with embodiment 1.
The NaHCO that in test water, adds different concns
3The pH value is adjusted to 7.5, add 5mg/L 1-Hydroxy Ethylidene-1,1-Diphosphonic Acid, 8mg/L Sodium orthomolybdate, 5mg/L vinylformic acid and the 2-acrylamide-copolymer of 2-methyl-propyl sulfonic acid, 5mg/L zinc chloride again, the erosion rate of rotary hanging plate is 0.031mm/a, and the erosion rate that does not add the rotary hanging plate of above-mentioned medicament is 1.32mm/a.
Embodiment 3
Present embodiment is the rotary hanging plate corrosion test, carries out with reference to HG/T2159-91.
Test water quality is with embodiment 1.
The NaHCO that in test water, adds different concns
3The pH value is adjusted to 10.5, add 5mg/L 2-phosphino--1 again, 2,4-tricarboxylic acid-butane, 10mg/L Sodium hexametaphosphate 99,8mg/L vinylformic acid and the 2-acrylamide-copolymer of 2-methyl-propyl sulfonic acid, 5mg/L zinc chloride, the erosion rate of rotary hanging plate is 0.021mm/a, and the erosion rate that does not add the rotary hanging plate of above-mentioned medicament is 1.32mm/a.
Embodiment 4
Present embodiment is a microbial inhibition assays.
Test water quality is with embodiment 1.
4 in beaker after the process sterilization, after adding on-the-spot supposition water purification 500mL respectively, the trichloroisocyanuric acid that in No. 2 beakers, adds 20mg/L, the benzyl dimethyl dodecyl chlorination ammonium that adds 50mg/L in No. 3 beakers, the benzyl dimethyl dodecyl chlorination ammonium and the 300mg/L sodium hydroxide that add 50mg/L in No. 4 beakers, above-mentioned medicament shakes up respectively after adding immediately, carry out Bacteria Detection, result such as table 2 according to 207,208,210 and 209 methods in " water coolant analysis and test method " (production department of China PetroChemical Corporation, development division) behind the effect 4h.
Table 2 bactericidal assay result
Embodiment 5
This example is a dynamic analog test.
Test water quality is with embodiment 1.
Test is carried out with reference to HG/T2160-91 standard " water coolant dynamic simulation experiment method ".The 20# carbon steel test tube of 2 φ 10 * 1 * 530mm carries out parallel test, and test water is walked tube side.The heating of test tube external application saturated vapor, 30 ± 1 ℃ of control test water inflow temperatures, 8 ℃ of exit port water temperature difference, the recirculated water cycles of concentration is controlled at 3.0～4.0, and 400h is carried out in test continuously.The erosion rate that obtains test tube is 0.037mm/a, adheres to speed 8.3mg/ (cm
2.mon.), in the process of the test recirculated water microorganism concn less than 10
4Individual/mL.
Claims (10)
1. one kind is fit to the treatment process that the supposition water purification is back to circulating water system, comprise: will suppose that water purification introduces circulating water system after oil removal, sedimentation, adding inorganic base substance makes recirculated water pH value reach 7.0～11, add sterilant and corrosion inhibiting and descaling agent, make its concentration in recirculated water be controlled at 1～100mg/L and 1～50mg/L respectively.
2. in accordance with the method for claim 1, it is characterized in that said alkaline matter is selected from NaOH, KOH, Na
2CO
3, K
2CO
3, NaHCO
3, KHCO
3One of or two or more mixture wherein.
3. in accordance with the method for claim 1, it is characterized in that said alkaline matter is NaHCO
3
4. in accordance with the method for claim 1, it is characterized in that recirculated water pH value is controlled at 7.5～10.0.
5. in accordance with the method for claim 1, it is characterized in that said sterilant is selected from one of chlorine, clorox, potassium hypochlorite, Losantin, DICHLOROISOCYANURIC ACID, trichloroisocyanuric acid, dioxide peroxide, bromine, sodium hypobromite, potassium hypobromite, hypobromous acid calcium, quaternary ammonium salt and quaternary alkylphosphonium salt or two or more mixture wherein.
6. in accordance with the method for claim 5, it is characterized in that said sterilant is selected from clorox, DICHLOROISOCYANURIC ACID and trichloroisocyanuric acid.
7. in accordance with the method for claim 1, it is characterized in that the concentration that adds of said sterilant is 2～50mg/L.
8. in accordance with the method for claim 1, it is characterized in that said corrosion inhibiting and descaling agent is selected from hydroxyl phosphino-acetate, 1-Hydroxy Ethylidene-1,1-Diphosphonic Acid, Sodium hexametaphosphate 99, zinc salt and molybdate.
9. in accordance with the method for claim 8, it is characterized in that said corrosion inhibiting and descaling agent is a hydroxyl phosphino-acetate.
10. in accordance with the method for claim 1, it is characterized in that said corrosion inhibiting and descaling agent adds concentration 3～15mg/L.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03105394 CN1232455C (en) | 2003-02-28 | 2003-02-28 | Treating method suitable for presumption of recycling pure water into circulating water system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 03105394 CN1232455C (en) | 2003-02-28 | 2003-02-28 | Treating method suitable for presumption of recycling pure water into circulating water system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1524806A true CN1524806A (en) | 2004-09-01 |
| CN1232455C CN1232455C (en) | 2005-12-21 |
Family
ID=34282644
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 03105394 Expired - Lifetime CN1232455C (en) | 2003-02-28 | 2003-02-28 | Treating method suitable for presumption of recycling pure water into circulating water system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1232455C (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102603034A (en) * | 2011-12-15 | 2012-07-25 | 汪洋 | Method and device for regulating quality of desalinated sea water |
| CN102730863A (en) * | 2011-04-02 | 2012-10-17 | 中国石油化工股份有限公司 | Method for treating light oil-leaking circulating water |
| CN103030238A (en) * | 2011-09-29 | 2013-04-10 | 中国石油化工股份有限公司 | Circulating water treatment method adopting deionized water as supplement water |
| CN103030227A (en) * | 2011-09-29 | 2013-04-10 | 中国石油化工股份有限公司 | Circulating water treatment method adopting deionized water as supplement water |
| CN103030240A (en) * | 2011-09-29 | 2013-04-10 | 中国石油化工股份有限公司 | Circulating water treatment method adopting deionized water as supplement water |
| US8759051B2 (en) | 2010-12-20 | 2014-06-24 | E I Du Pont De Nemours And Company | Control of contaminant microorganisms in fermentation processes with peroxygen-releasing compounds |
| CN104193029A (en) * | 2005-08-11 | 2014-12-10 | 热能公司 | Ammonium/ammonia removal from a stream |
| CN105217775A (en) * | 2015-11-17 | 2016-01-06 | 新疆德蓝股份有限公司 | A kind of water conditioner of quick removal ammonia nitrogen |
| CN109502774A (en) * | 2018-08-17 | 2019-03-22 | 滨州市丰泰技术开发有限公司 | A kind of manufacturing method of oil field composite multi-functional fungicide |
-
2003
- 2003-02-28 CN CN 03105394 patent/CN1232455C/en not_active Expired - Lifetime
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104193029A (en) * | 2005-08-11 | 2014-12-10 | 热能公司 | Ammonium/ammonia removal from a stream |
| US8759051B2 (en) | 2010-12-20 | 2014-06-24 | E I Du Pont De Nemours And Company | Control of contaminant microorganisms in fermentation processes with peroxygen-releasing compounds |
| CN102730863A (en) * | 2011-04-02 | 2012-10-17 | 中国石油化工股份有限公司 | Method for treating light oil-leaking circulating water |
| CN102730863B (en) * | 2011-04-02 | 2015-01-21 | 中国石油化工股份有限公司 | Method for treating light oil-leaking circulating water |
| CN103030238A (en) * | 2011-09-29 | 2013-04-10 | 中国石油化工股份有限公司 | Circulating water treatment method adopting deionized water as supplement water |
| CN103030227A (en) * | 2011-09-29 | 2013-04-10 | 中国石油化工股份有限公司 | Circulating water treatment method adopting deionized water as supplement water |
| CN103030240A (en) * | 2011-09-29 | 2013-04-10 | 中国石油化工股份有限公司 | Circulating water treatment method adopting deionized water as supplement water |
| CN103030227B (en) * | 2011-09-29 | 2014-12-17 | 中国石油化工股份有限公司 | Circulating water treatment method adopting deionized water as supplement water |
| CN103030238B (en) * | 2011-09-29 | 2015-08-05 | 中国石油化工股份有限公司 | A kind of deionized water does the circulating water treatment method of moisturizing |
| CN102603034A (en) * | 2011-12-15 | 2012-07-25 | 汪洋 | Method and device for regulating quality of desalinated sea water |
| CN105217775A (en) * | 2015-11-17 | 2016-01-06 | 新疆德蓝股份有限公司 | A kind of water conditioner of quick removal ammonia nitrogen |
| CN109502774A (en) * | 2018-08-17 | 2019-03-22 | 滨州市丰泰技术开发有限公司 | A kind of manufacturing method of oil field composite multi-functional fungicide |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1232455C (en) | 2005-12-21 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP4233479B2 (en) | Method and system for treatment of wastewater containing organic compounds | |
| WO2012155607A1 (en) | Apparatus for producing reclaimed water based on electrolysis and double membrane technologies and method thereof | |
| WO2012126316A2 (en) | Sewage recycling device based on electrolysis and mbr technologies and method thereof | |
| CN1724420A (en) | Process for combined water treatment of chemical oxidizing-biological biological filtering tank | |
| CN101041531A (en) | Multiple combined technique for high concentration hard-degraded organic waste water treatment | |
| CN100336737C (en) | Method of removing ammonia nitrogen in water by using electrodialysis | |
| KR101278230B1 (en) | The method and Appuratus of removing total nitrogen and phosphate in sewage and wastewater using precipitation-agent of rapidity for coagulation an flocculation | |
| Xu et al. | Roofing rainwater cleaner production using pilot-scale electrocoagulation coupled with a gravity-driven membrane bioreactor (EC-GDMBR): Water treatment and energy efficiency | |
| CN1232455C (en) | Treating method suitable for presumption of recycling pure water into circulating water system | |
| CN104291522A (en) | Method for treating industrial wastewater | |
| WO2011158195A1 (en) | Wastewater treatment comprising electrodissolution, flocculation and oxidation | |
| CN1323958C (en) | Method for processing urban sewage deeply | |
| CN2856037Y (en) | Sewage reclaiming treatment unit | |
| Priya et al. | Degradation studies of tannery effluents using electro flotation technique | |
| CN1733617A (en) | Processing method of waste water containing fluorine arsenic and lead | |
| WO2020020459A1 (en) | Anolyte as an additive for wastewater treatment | |
| WO2019200775A1 (en) | Wastewater circulating cleaning treatment method capable of reducing sludge amount | |
| CN207552128U (en) | A kind of device of integrated membrane process hydridization removal low concentration selenium-containing wastewater | |
| CN103253836B (en) | A kind of percolate deep purifying treatment unit and method | |
| CN108059308B (en) | Chloramphenicol wastewater pretreatment process | |
| CN1199890C (en) | Domestic sewage treating method and use | |
| EP3447030A1 (en) | Process of treatment of agroindustrial waste water by reaction of acidification with addition of strong acids | |
| CN110451635A (en) | A kind of biological treatment system and method for high organic matter industrial wastewater with high salt | |
| CN1693239A (en) | Tech. process for reducing mineralization of extracting oil sewage | |
| CN217459127U (en) | Strong brine waste water high-efficient nitrogen and phosphorus removal processing system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term |
Granted publication date: 20051221 |
|
| CX01 | Expiry of patent term |